Abstract
Hydrogasification of pinewood was studied in the presence of steam using a micro-batch reactor. A series of reaction experiments were performed at temperatures ranging from 873 to 1043 K, and pressures ranging from 5 to 35 bar. It was found that steam significantly increases not only the rate of the hydrogasification reaction but also the conversion of carbon into product gases. The enhancement of the formation of total carbon-containing gases (CH 4, CO, CO 2 and C 2+) by adding steam is estimated to be as high as 30 times greater compared to dry hydrogasification at 1043 K. Increased hydrogen pressure also enhanced methane formation in the product gas.
Sign-in/Register to access full text options 
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Schedule a callDisclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.
